Chemical Industry and Engineering Progress ›› 2021, Vol. 40 ›› Issue (10): 5491-5498.DOI: 10.16085/j.issn.1000-6613.2020-2225
• Chemical processes and equipment • Previous Articles Next Articles
LI Xingyan1(), WANG Mo1, DAI Xuan1, PENG Xinhua1, TANG Shuangling2()
Received:
2020-11-06
Revised:
2021-03-16
Online:
2021-10-25
Published:
2021-10-10
Contact:
TANG Shuangling
李星彦1(), 王墨1, 戴璇1, 彭新华1, 唐双凌2()
通讯作者:
唐双凌
作者简介:
李星彦(1996—),男,硕士研究生,研究方向为有机化学。E-mail:基金资助:
CLC Number:
LI Xingyan, WANG Mo, DAI Xuan, PENG Xinhua, TANG Shuangling. Nitration of n-hexane with NO2 and theoretical calculation[J]. Chemical Industry and Engineering Progress, 2021, 40(10): 5491-5498.
李星彦, 王墨, 戴璇, 彭新华, 唐双凌. NO2硝化正己烷及其理论计算[J]. 化工进展, 2021, 40(10): 5491-5498.
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序号 | 温度 /℃ | 转化率② /% | 选择性/% | ||
---|---|---|---|---|---|
1-硝基己烷 | 2-硝基己烷 | 3-硝基己烷 | |||
1 | 100 | 29.6 | 1.2 | 58.0 | 40.9 |
2 | 110 | 58.9 | 1.4 | 57.6 | 41.0 |
3 | 120 | 64.3 | 2.3 | 56.5 | 41.2 |
4 | 130 | 64.8 | 1.9 | 57.2 | 40.9 |
5 | 140 | 65.3 | 2.1 | 56.5 | 41.4 |
序号 | 温度 /℃ | 转化率② /% | 选择性/% | ||
---|---|---|---|---|---|
1-硝基己烷 | 2-硝基己烷 | 3-硝基己烷 | |||
1 | 100 | 29.6 | 1.2 | 58.0 | 40.9 |
2 | 110 | 58.9 | 1.4 | 57.6 | 41.0 |
3 | 120 | 64.3 | 2.3 | 56.5 | 41.2 |
4 | 130 | 64.8 | 1.9 | 57.2 | 40.9 |
5 | 140 | 65.3 | 2.1 | 56.5 | 41.4 |
序号 | 正己烷∶NO2 (摩尔比) | 转化率② /% | 选择性/% | ||
---|---|---|---|---|---|
1-硝基己烷 | 2-硝基己烷 | 3-硝基己烷 | |||
1 | 1∶0.5 | 32.0 | 1.3 | 55.9 | 42.9 |
2 | 1∶1 | 64.3 | 2.3 | 56.5 | 41.2 |
3 | 1∶1.5 | 73.0 | 2.7 | 57.0 | 41.4 |
4 | 1∶2 | 85.9 | 2.0 | 54.3 | 43.7 |
5 | 1∶2.5 | 86.1 | 1.8 | 52.2 | 46.0 |
序号 | 正己烷∶NO2 (摩尔比) | 转化率② /% | 选择性/% | ||
---|---|---|---|---|---|
1-硝基己烷 | 2-硝基己烷 | 3-硝基己烷 | |||
1 | 1∶0.5 | 32.0 | 1.3 | 55.9 | 42.9 |
2 | 1∶1 | 64.3 | 2.3 | 56.5 | 41.2 |
3 | 1∶1.5 | 73.0 | 2.7 | 57.0 | 41.4 |
4 | 1∶2 | 85.9 | 2.0 | 54.3 | 43.7 |
5 | 1∶2.5 | 86.1 | 1.8 | 52.2 | 46.0 |
进攻位置 | 总能量/kJ·mol-1 | ||
---|---|---|---|
途径(1) | 途径(2) | 途径(3) | |
1-C | |||
ER | -1160803.565 | -1160803.155 | -1160803.708 |
ETS | -1160694.314 | -1160701.600 | -1160538.883 |
Ea | 109.252 | 101.556 | 264.825 |
2-C | |||
ER | -1160803.595 | -1160803.618 | -1160799.290 |
ETS | -1160710.242 | -1160715.722 | -1160524.374 |
Ea | 93.354 | 87.896 | 274.916 |
3-C | |||
ER | -1160803.507 | -1160802.418 | -1160803.395 |
ETS | -1160708.007 | -1160713.692 | -1160532.478 |
Ea | 95.499 | 88.727 | 270.917 |
进攻位置 | 总能量/kJ·mol-1 | ||
---|---|---|---|
途径(1) | 途径(2) | 途径(3) | |
1-C | |||
ER | -1160803.565 | -1160803.155 | -1160803.708 |
ETS | -1160694.314 | -1160701.600 | -1160538.883 |
Ea | 109.252 | 101.556 | 264.825 |
2-C | |||
ER | -1160803.595 | -1160803.618 | -1160799.290 |
ETS | -1160710.242 | -1160715.722 | -1160524.374 |
Ea | 93.354 | 87.896 | 274.916 |
3-C | |||
ER | -1160803.507 | -1160802.418 | -1160803.395 |
ETS | -1160708.007 | -1160713.692 | -1160532.478 |
Ea | 95.499 | 88.727 | 270.917 |
几何参数 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) |
---|---|---|---|
键长/? C(1)—C(5) C(5)—C(8) C(8)—C(11) C(5)—H(6) C(5)—H(7) H(7)—O(22) O(22)—N(21) N(21)—O(23) | 1.531 1.532 1.537 1.097 1.089(0.3525) 1.991(0.0050) 1.205 1.204 | 1.508 1.511 1.536 1.095 1.412(0.1889) 1.190(0.0185) 1.319 1.205 | 1.496 1.499 1.538 1.091 1.988(0.0728) 1.009(0.1121) 1.372 1.197 |
键角/(°) C(1)—C(5)—C(8) C(5)—C(8)—C(11) C(8)—C(11)—C(14) C(11)—C(14)—C(17) C(1)—C(5)—H(7) C(8)—C(5)—H(7) | 115.4 113.0 113.3 113.7 109.0 107.8 | 118.3 114.6 113.2 113.0 104.1 103.2 | 121.6 114.2 113.3 113.1 98.3 100.5 |
二面角/(°) C(5)—N(21)—O(22)—O(23) H(7)—N(21)—O(22)—O(23) | -1.0 -7.7 | -0.9 -1.2 | -0.3 -0.9 |
几何参数 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) |
---|---|---|---|
键长/? C(1)—C(5) C(5)—C(8) C(8)—C(11) C(5)—H(6) C(5)—H(7) H(7)—O(22) O(22)—N(21) N(21)—O(23) | 1.531 1.532 1.537 1.097 1.089(0.3525) 1.991(0.0050) 1.205 1.204 | 1.508 1.511 1.536 1.095 1.412(0.1889) 1.190(0.0185) 1.319 1.205 | 1.496 1.499 1.538 1.091 1.988(0.0728) 1.009(0.1121) 1.372 1.197 |
键角/(°) C(1)—C(5)—C(8) C(5)—C(8)—C(11) C(8)—C(11)—C(14) C(11)—C(14)—C(17) C(1)—C(5)—H(7) C(8)—C(5)—H(7) | 115.4 113.0 113.3 113.7 109.0 107.8 | 118.3 114.6 113.2 113.0 104.1 103.2 | 121.6 114.2 113.3 113.1 98.3 100.5 |
二面角/(°) C(5)—N(21)—O(22)—O(23) H(7)—N(21)—O(22)—O(23) | -1.0 -7.7 | -0.9 -1.2 | -0.3 -0.9 |
原子 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) | 原子 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) |
---|---|---|---|---|---|---|---|
C(1) | -0.4413 | -0.4516 | -0.4750 | H(13) | 0.1241 | 0.1320 | 0.1320 |
H(2) | 0.1398 | 0.1604 | 0.1569 | C(14) | -0.2464 | -0.2500 | -0.2497 |
H(3) | 0.1405 | 0.1624 | 0.1612 | H(15) | 0.1289 | 0.1307 | 0.1311 |
H(4) | 0.1414 | 0.1758 | 0.1728 | H(16) | 0.1299 | 0.1347 | 0.1343 |
C(5) | -0.2490 | -0.2535 | -0.1665 | C(17) | -0.4413 | -0.4430 | -0.4431 |
H(6) | 0.1291 | 0.1722 | 0.1512 | H(18) | 0.1410 | 0.1468 | 0.1468 |
H(7) | 0.1230 | 0.3422 | 0.4022 | H(19) | 0.1405 | 0.1445 | 0.1442 |
C(8) | -0.2436 | -0.2546 | -0.2697 | H(20) | 0.1401 | 0.1429 | 0.1424 |
H(9) | 0.1250 | 0.1509 | 0.1475 | N(21) | 0.4838 | 0.3091 | 0.2935 |
H(10) | 0.1261 | 0.1484 | 0.1447 | O(22) | -0.2365 | -0.3971 | -0.4660 |
C(11) | -0.2494 | -0.2572 | -0.2590 | O(23) | -0.2340 | -0.2966 | -0.2765 |
H(12) | 0.1282 | 0.1508 | 0.1446 |
原子 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) | 原子 | 反应物(R) | 过渡态(TS2) | 中间体(IM2) |
---|---|---|---|---|---|---|---|
C(1) | -0.4413 | -0.4516 | -0.4750 | H(13) | 0.1241 | 0.1320 | 0.1320 |
H(2) | 0.1398 | 0.1604 | 0.1569 | C(14) | -0.2464 | -0.2500 | -0.2497 |
H(3) | 0.1405 | 0.1624 | 0.1612 | H(15) | 0.1289 | 0.1307 | 0.1311 |
H(4) | 0.1414 | 0.1758 | 0.1728 | H(16) | 0.1299 | 0.1347 | 0.1343 |
C(5) | -0.2490 | -0.2535 | -0.1665 | C(17) | -0.4413 | -0.4430 | -0.4431 |
H(6) | 0.1291 | 0.1722 | 0.1512 | H(18) | 0.1410 | 0.1468 | 0.1468 |
H(7) | 0.1230 | 0.3422 | 0.4022 | H(19) | 0.1405 | 0.1445 | 0.1442 |
C(8) | -0.2436 | -0.2546 | -0.2697 | H(20) | 0.1401 | 0.1429 | 0.1424 |
H(9) | 0.1250 | 0.1509 | 0.1475 | N(21) | 0.4838 | 0.3091 | 0.2935 |
H(10) | 0.1261 | 0.1484 | 0.1447 | O(22) | -0.2365 | -0.3971 | -0.4660 |
C(11) | -0.2494 | -0.2572 | -0.2590 | O(23) | -0.2340 | -0.2966 | -0.2765 |
H(12) | 0.1282 | 0.1508 | 0.1446 |
频率 | 反应物 | 过渡态 | 中间体 | 频率 | 反应物 | 过渡态 | 中间体 |
---|---|---|---|---|---|---|---|
υ1 | 5(0) | -1417(355) | 16(0) | υ33 | 1290(0) | 1209(18) | 1233(8) |
υ2 | 14(0) | 31(0) | 34(1) | υ34 | 1297(1) | 1231(16) | 1270(1) |
υ3 | 19(0) | 48(0) | 40(0) | υ35 | 1306(0) | 1272(3) | 1295(0) |
υ4 | 49(0) | 57(0) | 71(0) | υ36 | 1345(0) | 1294(1) | 1303(1) |
υ5 | 52(0) | 93(0) | 79(0) | υ37 | 1355(5) | 1299(1) | 1345(15) |
υ6 | 71(0) | 117(1) | 93(0) | υ38 | 1368(0) | 1341(3) | 1358(3) |
υ7 | 86(1) | 130(0) | 125(1) | υ39 | 1384(3) | 1358(1) | 1374(1) |
υ8 | 98(0) | 139(0) | 126(0) | υ40 | 1385(0) | 1369(1) | 1380(8) |
υ9 | 124(0) | 166(0) | 148(1) | υ41 | 1452(1) | 1374(10) | 1386(3) |
υ10 | 148(0) | 208(0) | 166(2) | υ42 | 1454(0) | 1385(2) | 1433(1) |
υ11 | 232(0) | 239(0) | 208(4) | υ43 | 1460(0) | 1433(0) | 1450(5) |
υ12 | 243(0) | 250(0) | 245(0) | υ44 | 1468(9) | 1450(7) | 1454(10) |
υ13 | 286(0) | 301(0) | 295(0) | υ45 | 1468(1) | 1457(0) | 1457(0) |
υ14 | 352(0) | 362(0) | 354(0) | υ46 | 1469(3) | 1459(5) | 1467(0) |
υ15 | 448(0) | 438(0) | 449(0) | υ47 | 1477(0) | 1467(1) | 1469(6) |
υ16 | 710(4) | 475(1) | 565(24) | υ48 | 1482(3) | 1469(6) | 1480(3) |
υ17 | 721(5) | 706(6) | 651(14) | υ49 | 1654(296) | 1480(3) | 1634(177) |
υ18 | 723(1) | 729(1) | 710(2) | υ50 | 2890(1) | 1571(270) | 2814(28) |
υ19 | 783(1) | 770(0) | 760(2) | υ51 | 2893(6) | 2844(16) | 2856(30) |
υ20 | 861(3) | 813(11) | 829(70) | υ52 | 2903(0) | 2890(17) | 2899(1) |
υ21 | 879(0) | 866(0) | 864(2) | υ53 | 2907(94) | 2901(3) | 2902(4) |
υ22 | 880(0) | 881(4) | 879(4) | υ54 | 2911(19) | 2907(32) | 2910(61) |
υ23 | 979(0) | 887(1) | 889(1) | υ55 | 2919(72) | 2921(13) | 2922(34) |
υ24 | 981(1) | 981(12) | 913(270) | υ56 | 2919(13) | 2923(48) | 2926(3) |
υ25 | 1017(0) | 989(2) | 965(1) | υ57 | 2920(2) | 2928(3) | 2945(14) |
υ26 | 1027(0) | 1025(13) | 986(0) | υ58 | 2935(1) | 2953(35) | 2949(43) |
υ27 | 1042(4) | 1036(16) | 1026(1) | υ59 | 2949(90) | 2963(12) | 2985(56) |
υ28 | 1122(0) | 1061(83) | 1036(4) | υ60 | 2981(15) | 2984(28) | 2990(41) |
υ29 | 1173(0) | 1078(3) | 1084(0) | υ61 | 2982(126) | 2985(50) | 2992(7) |
υ30 | 1217(0) | 1120(19) | 1095(2) | υ62 | 2985(46) | 2990(41) | 3016(44) |
υ31 | 1235(5) | 1140(10) | 1135(1) | υ63 | 2986(42) | 3012(19) | 3024(381) |
υ32 | 1272(0) | 1165(29) | 1199(0) |
频率 | 反应物 | 过渡态 | 中间体 | 频率 | 反应物 | 过渡态 | 中间体 |
---|---|---|---|---|---|---|---|
υ1 | 5(0) | -1417(355) | 16(0) | υ33 | 1290(0) | 1209(18) | 1233(8) |
υ2 | 14(0) | 31(0) | 34(1) | υ34 | 1297(1) | 1231(16) | 1270(1) |
υ3 | 19(0) | 48(0) | 40(0) | υ35 | 1306(0) | 1272(3) | 1295(0) |
υ4 | 49(0) | 57(0) | 71(0) | υ36 | 1345(0) | 1294(1) | 1303(1) |
υ5 | 52(0) | 93(0) | 79(0) | υ37 | 1355(5) | 1299(1) | 1345(15) |
υ6 | 71(0) | 117(1) | 93(0) | υ38 | 1368(0) | 1341(3) | 1358(3) |
υ7 | 86(1) | 130(0) | 125(1) | υ39 | 1384(3) | 1358(1) | 1374(1) |
υ8 | 98(0) | 139(0) | 126(0) | υ40 | 1385(0) | 1369(1) | 1380(8) |
υ9 | 124(0) | 166(0) | 148(1) | υ41 | 1452(1) | 1374(10) | 1386(3) |
υ10 | 148(0) | 208(0) | 166(2) | υ42 | 1454(0) | 1385(2) | 1433(1) |
υ11 | 232(0) | 239(0) | 208(4) | υ43 | 1460(0) | 1433(0) | 1450(5) |
υ12 | 243(0) | 250(0) | 245(0) | υ44 | 1468(9) | 1450(7) | 1454(10) |
υ13 | 286(0) | 301(0) | 295(0) | υ45 | 1468(1) | 1457(0) | 1457(0) |
υ14 | 352(0) | 362(0) | 354(0) | υ46 | 1469(3) | 1459(5) | 1467(0) |
υ15 | 448(0) | 438(0) | 449(0) | υ47 | 1477(0) | 1467(1) | 1469(6) |
υ16 | 710(4) | 475(1) | 565(24) | υ48 | 1482(3) | 1469(6) | 1480(3) |
υ17 | 721(5) | 706(6) | 651(14) | υ49 | 1654(296) | 1480(3) | 1634(177) |
υ18 | 723(1) | 729(1) | 710(2) | υ50 | 2890(1) | 1571(270) | 2814(28) |
υ19 | 783(1) | 770(0) | 760(2) | υ51 | 2893(6) | 2844(16) | 2856(30) |
υ20 | 861(3) | 813(11) | 829(70) | υ52 | 2903(0) | 2890(17) | 2899(1) |
υ21 | 879(0) | 866(0) | 864(2) | υ53 | 2907(94) | 2901(3) | 2902(4) |
υ22 | 880(0) | 881(4) | 879(4) | υ54 | 2911(19) | 2907(32) | 2910(61) |
υ23 | 979(0) | 887(1) | 889(1) | υ55 | 2919(72) | 2921(13) | 2922(34) |
υ24 | 981(1) | 981(12) | 913(270) | υ56 | 2919(13) | 2923(48) | 2926(3) |
υ25 | 1017(0) | 989(2) | 965(1) | υ57 | 2920(2) | 2928(3) | 2945(14) |
υ26 | 1027(0) | 1025(13) | 986(0) | υ58 | 2935(1) | 2953(35) | 2949(43) |
υ27 | 1042(4) | 1036(16) | 1026(1) | υ59 | 2949(90) | 2963(12) | 2985(56) |
υ28 | 1122(0) | 1061(83) | 1036(4) | υ60 | 2981(15) | 2984(28) | 2990(41) |
υ29 | 1173(0) | 1078(3) | 1084(0) | υ61 | 2982(126) | 2985(50) | 2992(7) |
υ30 | 1217(0) | 1120(19) | 1095(2) | υ62 | 2985(46) | 2990(41) | 3016(44) |
υ31 | 1235(5) | 1140(10) | 1135(1) | υ63 | 2986(42) | 3012(19) | 3024(381) |
υ32 | 1272(0) | 1165(29) | 1199(0) |
1 | SIMPSON M F, LAW J D. Nuclear fuel reprocessing[M]//Nuclear Energy. New York: Springer, 2018: 187-204. |
2 | 姜圣阶, 任凤仪, 等. 核燃料后处理工学[M]. 北京: 原子能出版社, 1995. |
JIANG Shengjie, REN Fengyi, et al. Nuclear fuel reprocessing engineering[M]. Beijing: Atomic Energy Press, 1995. | |
3 | COLVEN T J, NICHOLS G M, SIDDALL T H. TNX evaporator incident January 12, 1953. interim technical report[R]. Office of Scientific and Technical Information (OSTI), 1953. |
4 | DURANT W S. Red oil explosion at the Savannah river plant[R]. DPMS-83-142, Savannah River Laboratory: 1984. |
5 | SEGE G. Overconcentration in initial operation of uranium evaporator, 321 Building[R]. Office of Scientific and Technical Information (OSTI), 1953. |
6 | DAVIS W J, BALDWIN W H, MESERVEY A B. Chemistry of the intercycle evaporator incident of November 20, 1959[R]. Office of Scientific and Technical Information (OSTI), 1960. |
7 | ANDREEV G, ANTIPIN Y, BENNETT B, et al. The radiological accident in the reprocessing plant at Tomsk[R]. International Atomic Energy Agency, Austria: 1998. |
8 | MINCHER B J, MODOLO G, MEZYK S P. Review article: the effects of radiation chemistry on solvent extraction: 1. Conditions in acidic solution and a review of TBP radiolysis[J]. Solvent Extraction and Ion Exchange, 2009, 27(1): 1-25. |
9 | 许明霞. 乏燃料后处理厂“红油”爆炸安全分析[J]. 核安全, 2011(1): 22-27. |
XU Mingxia. Safety analysis on explosion of “red oils” in spent fuel reprocessing plants[J]. Nuclear safety, 2011(1): 22-27. | |
10 | KUMAR S, KUMAR R, KOGANTI S B. Studies on reaction runaways for Urex/Purex solvent-nitric acid and red-oil synthesis[C]//Oak Ridge National Laboratory,International Solvent Extraction Conference2008. 9ISEC-2008. Tucson, USA. 2008. |
11 | KUMAR S, SINHA P K, KAMACHI MUDALI U, et al. Thermal decomposition of red-oil/nitric acid mixtures in adiabatic conditions[J]. Journal of Radioanalytical and Nuclear Chemistry, 2011, 289(2): 545-549. |
12 | SMITHA V S, SURIANARAYANAN M, SESHADRI H, et al. Thermal behavior pattern of tributyl phosphate under adiabatic conditions[J]. Journal of Thermal Analysis and Calorimetry, 2013, 111(1): 849-856. |
13 | CHANDRAN K, SAHOO T K, MURALIDARAN P, et al. Calorimetric studies on the thermal decomposition of tri n-butyl phosphate-nitric acid systems[J]. Journal of Thermal Analysis and Calorimetry, 2012, 110(2): 879-890. |
14 | TALLENT O K, MAILEN J C, DODSON K E. Purex diluent chemical degradation[J]. Nuclear Technology, 1985, 71(2): 417-425. |
15 | ISHIHARA T, OHWADA K. Chemical degradation of kerosene diluent with nitric acid[J]. Journal of Nuclear Science and Technology, 2008, 3(1): 20-26. |
16 | OHWADA K. On the identification of hydroxamic acids formed by nitric acid degradation of kerosene and i-dodecane[J]. Journal of Nuclear Science and Technology, 1968, 5(4): 163-167. |
17 | 周春俐, 王墨, 唐洪彬, 等. 正己烷与正十二烷在硝酸体系中的化学行为[J]. 核化学与放射化学, 2021, 43(2): 122-128. |
ZHOU Chunli, WANG Mo, TANG Hongbin, et al. Chemical behavior of n-hexane and n-dodecane in nitric acid system[J]. Journal of Nuclear and Radiochemistry, 2021, 43(2): 122-128. | |
18 | WAGNER R M. Investigation of explosive characteristics of purex solvent decomposition products (Red oil)[R]. Office of Scientific and Technical Information (OSTI), 1953. |
19 | WILBOURN R G. Safety aspects of solvent nitration in HTGR fuel reprocessing[R]. Office of Scientific and Technical Information (OSTI), 1977. |
20 | HOU Y, BAREFIELD E K, TEDDER D W, et al. Thermal decomposition of nitrated tributyl phosphate[J]. Nuclear Technology, 1996, 113(3): 304-315. |
21 | SAKAGUCHI S, NISHIWAKI Y, KITAMURA T, et al. Efficient catalytic alkane nitration with NO2 under air assisted by N-hydroxyphthalimide[J]. Angewandte Chemie International Edition, 2001, 40(1): 222-224. |
22 | NISHIWAKI Y, SAKAGUCHI S, ISHII Y. An efficient nitration of light alkanes and the alkyl side-chain of aromatic compounds with nitrogen dioxide and nitric acid catalyzed by N-hydroxyphthalimide[J]. The Journal of Organic Chemistry, 2002, 67(16): 5663-5668. |
23 | SUZUKI H, MURASHIMA T, KOZAI I, et al. Ozone-mediated nitration of alkylbenzenes and related compounds with nitrogen dioxide[J]. Journal of the Chemical Society, Perkin Transactions 1, 1993(14): 1591. |
24 | PENG X, SUZUKI H, LU C. Zeolite-assisted nitration of neat toluene and chlorobenzene with a nitrogen dioxide/molecular oxygen system. Remarkable enhancement of para-selectivity[J]. Tetrahedron Letters, 2001, 42(26): 4357-4359. |
25 | DONG J, JIN B, SUN P. Palladium-catalyzed direct ortho-nitration of azoarenes using NO2 as nitro source[J]. Organic Letters, 2014, 16(17): 4540-4542. |
26 | 许晓娟, 肖鹤鸣, 贡雪东, 等. NO2气相硝化金刚烷的计算研究[J]. 化学学报, 2006, 64(4): 306-312. |
XU Xiaojuan, XIAO Heming, GONG Xuedong, et al. Computational studies on the nitration of adamantane with NO2[J]. Acta Chimica Sinica, 2006, 64(4): 306-312. |
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